Molecular sieve SSZ-100

ABSTRACT

A new crystalline molecular sieve designated SSZ-100 is disclosed. SSZ-100 is synthesized using a cationic nitrogen-containing organic compound having the following structure:

TECHNICAL FIELD

This disclosure relates to a new crystalline molecular sieve designatedSSZ-100, a method for preparing SSZ-100, and uses for SSZ-100.

BACKGROUND

Molecular sieve materials, both natural and synthetic, have beendemonstrated in the past to be useful as adsorbents and to havecatalytic properties for various types of hydrocarbon conversionreactions. Certain molecular sieves, such as zeolites,aluminophosphates, and mesoporous materials, are ordered, porouscrystalline materials having a definite crystalline structure asdetermined by X-ray diffraction (XRD). Within the crystalline molecularsieve material there are a large number of cavities which may beinterconnected by a number of channels or pores. These cavities andpores are uniform in size within a specific molecular sieve material.Because the dimensions of these pores are such as to accept foradsorption molecules of certain dimensions while rejecting those oflarger dimensions, these materials have come to be known as “molecularsieves” and are utilized in a variety of industrial processes.

Although many different crystalline molecular sieves have beendiscovered, there is a continuing need for new molecular sieves withdesirable properties for gas separation and drying, hydrocarbonconversion reactions, and other applications. New molecular sieves cancontain novel internal pore architectures, providing enhancedselectivities in these processes.

U.S. Pat. No. 4,910,006 discloses the synthesis of molecular sieveSSZ-26 using a hexamethyl[4.3.3.0]propellane-8,11-diammonium cation asstructure directing agent (“SDA”). In the synthesis of this SDA from[4.3.3.0]propellane-8,11-dione, it was reported that a small amount of amono-amine impurity was also produced in the reaction sequence. Themono-amine could be carried through all steps of the synthesis of theSDA without adversely affecting the synthesis of SSZ-26.

It has now been found that this reported mono-amine impurity is a monoquaternary ammonium compound, and when used as a structure directingagent, produces a unique molecular sieve material designated SSZ-100.

SUMMARY

The present disclosure is directed to a new family of molecular sieveswith unique properties, referred to herein as “molecular sieve SSZ-100”or simply “SSZ-100.”

In one aspect, there is provided a molecular sieve having a mole ratioof at least 10 of (1) at least one oxide of at least one tetravalentelement to (2) optionally, one or more oxides selected from the groupconsisting of oxides of trivalent elements, pentavalent elements, andmixtures thereof, and having, in its as-synthesized form, the X-raydiffraction lines of Table 5. It should be noted that the phrase “moleratio of at least 10” includes the case where there is no oxide (2),i.e., the mole ratio of oxide (1) to oxide (2) is infinity. In thatcase, the molecular sieve is comprised of essentially all of the oxideof the one or more tetravalent elements.

In another aspect, there is provided a method of preparing a crystallinemolecular sieve by contacting under crystallization conditions (1) atleast one source of an oxide of at least one tetravalent element; (2)optionally, one or more sources of one or more oxides selected from thegroup consisting of oxides of trivalent elements, pentavalent elements,and mixtures thereof; (3) at least one source of an element selectedfrom Groups 1 and 2 of the Periodic Table; (4) hydroxide ions; and (5) acationic nitrogen-containing organic compound represented by thefollowing structure:

In yet another aspect, there is provided a process for preparing acrystalline molecular sieve having, in its as-synthesized form, theX-ray diffraction lines of Table 5, by: (a) preparing a reaction mixturecontaining (1) at least one source of an oxide of at least onetetravalent element; (2) optionally, one or more sources of one or moreoxides selected from the group consisting of oxides of trivalentelements, pentavalent elements, and mixtures thereof; (3) at least onesource of an element selected from Groups 1 and 2 of the Periodic Table;(4) hydroxide ions; (5) water; and (6) a cationic nitrogen-containingorganic compound represented by the following structure:

and (b) subjecting the reaction mixture to crystallization conditionssufficient to form crystals of the molecular sieve.

The present disclosure also provides SSZ-100 molecular sieves having acomposition, as-synthesized and in the anhydrous state, in terms of moleratios, as follows:

Broad Exemplary TO₂/X₂O_(b) ≧10  10 to 100 Q/TO₂ 0.02 to 0.10 0.02 to0.10 M/TO₂ 0.02 to 0.15 0.02 to 0.15wherein: (1) T is selected from the group consisting of tetravalentelements from Groups 4-14 of the Periodic Table, and mixtures thereof;(2) X is selected from the group consisting of trivalent and pentavalentelements from Groups 3-13 of the Periodic Table, and mixtures thereof;(3) stoichiometric variable b equals the valence state of compositionalvariable X (e.g., when X is trivalent, b=3; when X is pentavalent, b=5);(4) M is selected from the group consisting of elements from Groups 1and 2 of the Periodic Table; and (5) Q is a cationic nitrogen-containingorganic compound represented by the following structure:

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 depicts the structure of the SDA prepared in Example 1 drawn with30% thermal ellipsoids as determined by single-crystal X-raydiffraction.

FIG. 2 is a powder XRD pattern of the as-synthesized molecular sieveprepared in Example 2.

FIG. 3 is a powder XRD pattern of the calcined molecular sieve preparedin Example 3.

DETAILED DESCRIPTION Introduction

The term “molecular sieve” includes (a) intermediate and (b) final ortarget molecular sieves and molecular sieves produced by (1) directsynthesis or (2) post-crystallization treatment (secondary synthesis).Secondary synthesis techniques allow for the synthesis of a targetmaterial from an intermediate material by heteroatom latticesubstitution or other techniques. For example, an aluminosilicate can besynthesized from an intermediate borosilicate by post-crystallizationheteroatom lattice substitution of the boron for aluminum. Suchtechniques are known, for example as described in U.S. Pat. No.6,790,433.

As used herein, the numbering scheme for the Periodic Table Groups is asdisclosed in Chem. Eng. News, 63(5), 27 (1985).

In preparing SSZ-100, a cationic nitrogen-containing organic compoundrepresented by the flowing structure (1) is used as the structuredirecting agent (“SDA”), also known as a crystallization template:

The SDA cation is associated with anions which can be any anion that isnot detrimental to the formation of SSZ-100. Representative anionsinclude elements from Group 17 of the Periodic Table (e.g., fluoride,chloride, bromide and iodide), hydroxide, acetate, sulfate,tetrafluoroborate, carboxylate, and the like.

Reaction Mixture

In general, molecular sieve SSZ-100 is prepared by: (a) preparing areaction mixture containing (1) at least one source of an oxide of atleast one tetravalent element; (2) optionally, one or more sources ofone or more oxides selected from the group consisting of oxides oftrivalent elements, pentavalent elements, and mixtures thereof; (3) atleast one source of an element selected from Groups 1 and 2 of thePeriodic Table; (4) hydroxide ions; (5) water; and (6) a cationicnitrogen-containing organic compound represented by the followingstructure

and (b) subjecting the reaction mixture to crystallization conditionssufficient to form crystals of the molecular sieve.

The composition of the reaction mixture from which the molecular sieveis formed, in terms of mole ratios, is identified in Table 1 below,wherein compositional variables T, X, M, and Q and stoichiometricvariable b are as described herein above.

TABLE 1 Components Broad Exemplary TO₂/X₂O_(b) ≧10  10 to 100 M/TO₂ 0.05to 0.50 0.15 to 0.30 Q/TO₂ 0.05 to 0.50 0.05 to 0.25 OH/TO₂ 0.10 to 1.0 0.10 to 0.50 H₂O/TO₂  15 to 300 25 to 60

In one sub-embodiment, the composition of the reaction mixture fromwhich SSZ-100 is formed, in terms of mole ratios, is identified in Table2 below, wherein compositional variables M and Q are as described hereinabove.

TABLE 2 Components Broad Exemplary SiO₂/Al₂O₃ ≧10  10 to 100 M/SiO₂ 0.05to 0.50 0.15 to 0.30 Q/SiO₂ 0.05 to 0.50 0.05 to 0.25 OH/SiO₂ 0.10 to1.0  0.10 to 0.50 H₂O/SiO₂  15 to 300 25 to 60

As noted above, for each embodiment described herein, T is selected fromthe group consisting of tetravalent elements from Groups 4-14 of thePeriodic Table. In one sub-embodiment, T is selected from the groupconsisting of silicon (Si), germanium (Ge), titanium (Ti), and mixturesthereof. In another sub-embodiment, T is selected from the groupconsisting of Si, Ge, and mixtures thereof. In one sub-embodiment, T isSi. Sources of elements selected for compositional variable T includeoxides, hydroxides, acetates, oxalates, ammonium salts and sulfates ofthe element(s) selected for T. In one sub-embodiment, each source(s) ofthe element(s) selected for composition variable T is an oxide. Where Tis Si, sources useful for Si include fumed silica, precipitatedsilicates, silica hydrogel, silicic acid, colloidal silica, tetra-alkylorthosilicates (e.g., tetraethyl orthosilicate), and silica hydroxides.Sources useful herein for Ge include germanium oxide and germaniumethoxide.

For each embodiment described herein, X is selected from the groupconsisting of trivalent and pentavalent elements from Groups 3-13 of thePeriodic Table. In one sub-embodiment, X is selected from the groupconsisting of boron (B), aluminum (Al), gallium (Ga), indium (In), iron(Fe), and mixtures thereof. In another sub-embodiment, X is selectedfrom the group consisting of B, Al, Ga, In, and mixtures thereof. In onesub-embodiment X is Al. Sources of elements selected for compositionalvariable X include oxides, hydroxides, acetates, oxalates, ammoniumsalts and sulfates of the element(s) selected for X. Where X is Al,sources useful for Al include aluminates, alumina, and aluminumcompounds such as AlCl₃, Al₂(SO₄)₃, Al(OH)₃, kaolin clays, and otherzeolites. An example of the source of aluminum oxide is LZ-210 zeolite(a type of Y zeolite). Boron, gallium, indium, titanium, and iron can beadded in forms corresponding to their aluminum and silicon counterparts.

As described herein above, for each embodiment described herein, thereaction mixture can be formed using at least one source of an elementselected from Groups 1 and 2 of the Periodic Table (referred to hereinas M). In one sub-embodiment, the reaction mixture is formed using asource of an element from Group 1 of the Periodic Table. In anothersub-embodiment, the reaction mixture is formed using a source of sodium(Na). Any M-containing compound which is not detrimental to thecrystallization process is suitable. Sources for such Groups 1 and 2elements include oxides, hydroxides, nitrates, sulfates, halides,oxalates, citrates and acetates thereof.

For each embodiment described herein, the molecular sieve reactionmixture can be supplied by more than one source. Also, two or morereaction components can be provided by one source.

The reaction mixture can be prepared either batch wise or continuously.Crystal size, morphology and crystallization time of the molecular sievedescribed herein can vary with the nature of the reaction mixture andthe crystallization conditions.

Crystallization and Post-Synthesis Treatment

In practice, the molecular sieve is prepared by: (a) preparing areaction mixture as described herein above; and (b) subjecting thereaction mixture to crystallization conditions sufficient to formcrystals of the molecular sieve.

The reaction mixture is maintained at an elevated temperature until thecrystals of the molecular sieve are formed. The hydrothermalcrystallization is usually conducted under pressure, and usually in anautoclave so that the reaction mixture is subject to autogenouspressure, at a temperature between 125° C. and 200° C.

The reaction mixture can be subjected to mild stirring or agitationduring the crystallization step. It will be understood by the skilledartisan that the molecular sieves described herein can containimpurities, such as amorphous materials, unit cells having frameworktopologies which do not coincide with the molecular sieve, and/or otherimpurities (e.g., organic hydrocarbons).

During the hydrothermal crystallization step, the molecular sievecrystals can be allowed to nucleate spontaneously from the reactionmixture. The use of crystals of the molecular sieve as seed material canbe advantageous in decreasing the time necessary for completecrystallization to occur. In addition, seeding can lead to an increasedpurity of the product obtained by promoting the nucleation and/orformation of the molecular sieve over any undesired phases. When used asseeds, seed crystals are added in an amount between 1% and 10% of theweight of the source for compositional variable T used in the reactionmixture.

Once the molecular sieve crystals have formed, the solid product isseparated from the reaction mixture by standard mechanical separationtechniques such as filtration. The crystals are water-washed and thendried to obtain the as-synthesized molecular sieve crystals. The dryingstep can be performed at atmospheric pressure or under vacuum.

The molecular sieve can be used as-synthesized, but typically will bethermally treated (calcined). The term “as-synthesized” refers to themolecular sieve in its form after crystallization, prior to removal ofthe SDA cation. The SDA can be removed by thermal treatment (e.g.,calcination), preferably in an oxidative atmosphere (e.g., air, gas withan oxygen partial pressure of greater than 0 kPa) at a temperaturereadily determinable by the skilled artisan sufficient to remove the SDAfrom the molecular sieve. The SDA can also be removed by photolysistechniques (e.g., exposing the SDA-containing molecular sieve product tolight or electromagnetic radiation that has a wavelength shorter thanvisible light under conditions sufficient to selectively remove theorganic compound from the molecular sieve) as described in U.S. Pat. No.6,960,327.

The molecular sieve can subsequently be calcined in steam, air or inertgas at temperatures ranging from 200° C. to 800° C. for periods of timeranging from 1 to 48 hours, or more. Usually, it is desirable to removethe extra-framework cation (e.g., Na⁺) by ion exchange and replace itwith hydrogen, ammonium, or any desired metal-ion.

Where the molecular sieve formed is an intermediate material, the targetmolecular sieve can be achieved using post-synthesis techniques such asheteroatom lattice substitution techniques. The target molecular sievecan also be achieved by removing heteroatoms from the lattice by knowntechniques such as acid leaching.

The molecular sieve made from the process disclosed herein can be formedinto a wide variety of physical shapes. Generally speaking, themolecular sieve can be in the form of a powder, a granule, or a moldedproduct, such as extrudate having a particle size sufficient to passthrough a 2-mesh (Tyler) screen and be retained on a 400-mesh (Tyler)screen. In cases where the catalyst is molded, such as by extrusion withan organic binder, the molecular sieve can be extruded before drying ordried (or partially dried) and then extruded.

The molecular sieve can be composited with other materials resistant tothe temperatures and other conditions employed in organic conversionprocesses. Such matrix materials include active and inactive materialsand synthetic or naturally occurring zeolites as well as inorganicmaterials such as clays, silica and metal oxides. Examples of suchmaterials and the manner in which they can be used are disclosed in U.S.Pat. Nos. 4,910,006 and 5,316,753.

Characterization of the Molecular Sieve

Molecular sieves made by the process disclosed herein have acomposition, as-synthesized and in the anhydrous state, as described inTable 3 (in terms of mole ratios), wherein compositional variables T, X,Q and M and stoichiometric variable b are as described herein above:

TABLE 3 Broad Exemplary TO₂/X₂O_(b) ≧10  10 to 100 Q/TO₂ 0.02 to 0.100.02 to 0.10 M/TO₂ 0.02 to 0.15 0.02 to 0.15

In one sub-embodiment, the molecular sieves made by the processdisclosed herein have a composition, as-synthesized and in the anhydrousstate, as described in Table 4 (in terms of mole ratios), whereincompositional variables Q and M are as described herein above:

TABLE 4 Broad Exemplary SiO₂/Al₂O₃ ≧10  10 to 100 Q/SiO₂ 0.02 to 0.100.02 to 0.10 M/SiO₂ 0.02 to 0.15 0.02 to 0.15

Molecular sieves synthesized by the process disclosed herein arecharacterized by their XRD pattern. The X-ray diffraction pattern linesof Table 5 are representative of as-synthesized SSZ-100 made inaccordance with this disclosure. Minor variations in the diffractionpattern can result from variations in the mole ratios of the frameworkspecies of the particular sample due to changes in lattice constants. Inaddition, sufficiently small crystals will affect the shape andintensity of peaks, leading to significant peak broadening. Minorvariations in the diffraction pattern can also result from variations inthe organic compound used in the preparation. Calcination can also causeminor shifts in the XRD pattern. Notwithstanding these minorperturbations, the basic crystal lattice structure remains unchanged.

TABLE 5 Characteristic Peaks for As-Synthesized SSZ-100 2-Theta^((a))d-Spacing, nm Relative Intensity^((b)) 8.50 1.039 M 8.99 0.983 S 9.990.885 M 12.43 0.712 W 14.06 0.630 W 15.88 0.558 VS 17.68 0.501 VS 18.560.478 VS 19.35 0.458 VS 19.94 0.445 VS 20.87 0.425 W 22.80 0.390 M 23.360.381 W 24.74 0.360 M 24.99 0.356 VS ^((a))±0.20 ^((b))The powder XRDpatterns provided are based on a relative intensity scale in which thestrongest line in the X-ray pattern is assigned a value of 100: W = weak(>0 to ≦20); M = medium (>20 to ≦40); S = strong (>40 to ≦60); VS = verystrong (>60 to ≦100).

The X-ray diffraction pattern lines of Table 6 are representative ofcalcined SSZ-100 made in accordance with this disclosure.

TABLE 6 Characteristic Peaks for Calcined SSZ-100 2-Theta^((a))d-Spacing, nm Relative Intensity^((b)) 8.48 1.041 VS 8.98 0.984 VS 10.040.880 S 12.38 0.714 W 14.17 0.625 W 15.85 0.559 S 17.07 0.519 W 17.640.503 M 18.68 0.475 S 19.44 0.456 W 19.78 0.449 M 19.98 0.444 S 20.220.439 W 21.30 0.417 W 22.80 0.390 M 23.06 0.385 M 24.29 0.366 W 24.990.356 VS ^((a))±0.20 ^((b))The powder XRD patterns provided are based ona relative intensity scale in which the strongest line in the X-raypattern is assigned a value of 100: W = weak (>0 to ≦20); M = medium(>20 to ≦40); S = strong (>40 to ≦60); VS = very strong (>60 to ≦100).

The powder X-ray diffraction patterns presented herein were collected bystandard techniques. The radiation was CuK_(α) radiation. The peakheights and the positions, as a function of 2θ where θ is the Braggangle, were read from the relative intensities of the peaks (adjustingfor background), and d, the interplanar spacing corresponding to therecorded lines, can be calculated.

Processes Using SSZ-100

SSZ-100 is useful as an adsorbent for gas separations. SSZ-100 can alsobe used as a catalyst for converting oxygenates (e.g., methanol) toolefins and for making small amines. SSZ-100 can be used to reduceoxides of nitrogen in a gas streams, such as automobile exhaust. SSZ-100can also be used to as a cold start hydrocarbon trap in combustionengine pollution control systems. SSZ-100 is particularly useful fortrapping C₃ fragments.

EXAMPLES

The following illustrative examples are intended to be non-limiting.

Example 1 Synthesis of SDA

The SDA was prepared according to Zones et al., J. Am. Chem. Soc. 1992,114, 4195-4201. The SDA can be isolated as eluting faster off a columnthan the diquaternary SDA used for synthesizing SSZ-26. The iodideproduct was then hydroxide-exchanged by dissolving the solid in a 5-foldmass excess of water, adding a 2.5-fold mass excess of AG® 1-X8 anionexchange resin (Bio-Rad Laboratories), and allowing the ion-exchange tooccur overnight. The solution was filtered and the resin was washed withanother ¼^(th) proportion (relative to the start) of water. The combinedaqueous fractions were titrated with 0.1N HCl to determine the hydroxideconcentration.

The molecular structure of the SDA was determined by single-crystalX-ray diffraction using standard techniques and is depicted in FIG. 1.

Example 2 Synthesis of SSZ-100

CAB-O-SIL® M5 fumed silica (Cabot Corp.), a FAU zeolite (SiO₂/Al₂O₃ moleratio=5), a hydroxide solution of the SDA synthesized per Example 1, 1 NNaOH, and deionized were mixed together in a Teflon liner. Thecomposition of the reaction mixture, in terms of mole ratios, isreported in Table 7.

TABLE 7 Reaction Mixture Composition SiO₂/Al₂O₃ 35 Q/SiO₂ 0.20 OH/SiO₂0.15 H₂O/SiO₂ 30

The Teflon liner was then capped and sealed within a steel Parrautoclave. The autoclave was placed on a spit within a convection ovenat 160° C. The autoclave was tumbled at 43 rpm for a week in the heatedoven. The autoclave was then removed and allowed to cool to roomtemperature. The solids were then recovered by filtration and washedthoroughly with deionized water. The solids were allowed to dry at roomtemperature.

The powder XRD pattern of the resulting product is shown in FIG. 2.

Elemental analysis indicated the product contained 33.2% Si and 2.67%Al.

Example 3 Calcination of SSZ-100

The resulting product was calcined inside a muffle furnace under a flowof air heated to 595° C. at a rate of 1° C./minute and held at 595° C.for 5 hours, cooled and then analyzed by powder XRD. The powder XRDpattern of the resulting product is shown in FIG. 3. The powder XRDpattern indicates that the material remains stable after calcination toremove the organic SDA.

Example 3 Micropore Volume Analysis

Calcined SSZ-100 was subjected to a surface area and micropore volumeanalysis using N₂ as adsorbate and via the BET method. The zeoliteexhibited a considerable void volume with a micropore volume of 0.22cm³/g. This is consistent with the SDA filling about 18 wt. % for theas-synthesized SSZ-100.

No n-hexane uptake for calcined SSZ-100 was observed at room temperatureindicating that SSZ-100 is a small pore molecular sieve (i.e., amolecular sieve having a pore size of from 3 Å to less than 5.0 Å).

Example 4 Ammonium-Ion Exchange of SSZ-100

The Na⁺ form of calcined SSZ-100 was converted to the NH₄ ⁺ form ofSSZ-100 by heating the material in an aqueous solution of NH₄NO₃(typically, 1 g of NH₄NO₃/1 g of SSZ-100 in 20 mL of deionized H₂O) at90° C. for 2-3 hours. The mixture was then filtered and the step wasrepeated as many times as desired (usually done 2-3 times). Afterfiltration, the obtained NH₄ ⁺-exchanged product was washed withdeionized water and air dried. The NH₄ ⁺ form of SSZ-100 can beconverted to the H form by calcination to 540° C.

Example 5 Constraint Index Test

The H⁺ form of SSZ-100 prepared per Example 4 was pelletized at 4 kpsi,crushed and granulated to 20-40 mesh. A 0.6 g sample of the granulatedmaterial was calcined in air at 540° C. for 4 hours and cooled in adesiccator to ensure dryness. Then, 0.47 g of material was packed into a¼ inch stainless steel tube with alundum on both sides of the molecularsieve bed. A furnace (Applied Test Systems, Inc.) was used to heat thereactor tube. Nitrogen was introduced into the reactor tube at 9.4mL/min and at atmospheric pressure. The reactor was heated to about 800°F. (427° C.), and a 50/50 feed of n-hexane and 3-methylpentane wasintroduced into the reactor at a rate of 8 μL/min. The feed wasdelivered by an ISCO pump. Direct sampling into a GC began after 15minutes of feed introduction. Test data results after 15 minutes onstream (800° F.) are presented in Table 8.

TABLE 8 Constraint Index Test Results n-Hexane Conversion (%) 11.2 3-MPConversion (%) 0.3 Feed Conversion (%) 5.7 Constraint Index (excluding2-MP) 35.29 Constraint Index (including 2-MP) 63.66 MP = methylpentane

For the purposes of this specification and appended claims, unlessotherwise indicated, all numbers expressing quantities, percentages orproportions, and other numerical values used in the specification andclaims, are to be understood as being modified in all instances by theterm “about.” Accordingly, unless indicated to the contrary, thenumerical parameters set forth in the following specification andattached claims are approximations that can vary depending upon thedesired properties sought to be obtained. It is noted that, as used inthis specification and the appended claims, the singular forms “a,”“an,” and “the,” include plural references unless expressly andunequivocally limited to one referent. As used herein, the term“include” and its grammatical variants are intended to be non-limiting,such that recitation of items in a list is not to the exclusion of otherlike items that can be substituted or added to the listed items. As usedherein, the term “comprising” means including elements or steps that areidentified following that term, but any such elements or steps are notexhaustive, and an embodiment can include other elements or steps.

Unless otherwise specified, the recitation of a genus of elements,materials or other components, from which an individual component ormixture of components can be selected, is intended to include allpossible sub-generic combinations of the listed components and mixturesthereof.

The patentable scope is defined by the claims, and can include otherexamples that occur to those skilled in the art. Such other examples areintended to be within the scope of the claims if they have structuralelements that do not differ from the literal language of the claims, orif they include equivalent structural elements with insubstantialdifferences from the literal languages of the claims. To an extent notinconsistent herewith, all citations referred to herein are herebyincorporated by reference.

The invention claimed is:
 1. A molecular sieve having a mole ratio of atleast 10 of (1) at least one oxide of at least one tetravalent elementto (2) one or more oxides selected from the group consisting oftrivalent elements, pentavalent elements, and mixtures thereof, andhaving, in its as-synthesized form, an X-ray diffraction patternsubstantially as shown in the following Table: 2-Theta d-Spacing, nmRelative Intensity  8.50 ± 0.20 1.039 M  8.99 ± 0.20 0.983 S  9.99 ±0.20 0.885 M 12.43 ± 0.20 0.712 W 14.06 ± 0.20 0.630 W 15.88 ± 0.200.558 VS 17.68 ± 0.20 0.501 VS 18.56 ± 0.20 0.478 VS 19.35 ± 0.20 0.458VS 19.94 ± 0.20 0.445 VS 20.87 ± 0.20 0.425 W 22.80 ± 0.20 0.390 M 23.36± 0.20 0.381 W 24.74 ± 0.20 0.360 M 24.99 ± 0.20 0.356 VS.


2. The molecular sieve of claim 1, wherein the molecular sieve has acomposition, as-synthesized and in its anhydrous state, in terms of moleratios, as follows: TO₂/X₂O_(b) ≧10 Q/TO₂ 0.02 to 0.10 M/TO₂ 0.02 to0.15

wherein: (1) T is selected from the group consisting of tetravalentelements from Groups 4-14 of the Periodic Table, and mixtures thereof;(2) X is selected from the group consisting of trivalent and pentavalentelements from Groups 3-13 of the Periodic Table, and mixtures thereof;(3) b equals the valence state of X; (4) M is selected from the groupconsisting of elements from Groups 1 and 2 of the Periodic Table; and(5) Q is a cationic nitrogen-containing organic compound represented bythe following structure:


3. The molecular sieve of claim 2, wherein T is selected from the groupconsisting of Si, Ge, and mixtures thereof.
 4. The molecular sieve ofclaim 3, wherein T is Si.
 5. The molecular sieve of claim 2, wherein Xis selected from the group consisting of B, Al, Ga, In, Fe, and mixturesthereof.
 6. The molecular sieve of claim 5, wherein X is selected fromthe group consisting of B, Al, Ga, In, and mixtures thereof.
 7. Themolecular sieve of claim 2, wherein T is Si and X is Al.
 8. Themolecular sieve of claim 2, wherein the molecular sieve has acomposition, as-synthesized and in its anhydrous state, in terms of moleratios, as follows: TO₂/X₂O_(b)  10 to 100 Q/TO₂ 0.02 to 0.10  M/TO₂0.02 to 0.15.


9. A molecular sieve having a mole ratio of at least 10 of (1) at leastone oxide of at least one tetravalent element to (2) one or more oxidesselected from the group consisting of trivalent elements, pentavalentelements, and mixtures thereof, and having, in its calcined form, anX-ray diffraction pattern substantially as shown in the following Table:2-Theta d-Spacing, nm Relative Intensity  8.48 ± 0.20 1.041 VS  8.98 ±0.20 0.984 VS 10.04 ± 0.20 0.880 S 12.38 ± 0.20 0.714 W 14.17 ± 0.200.625 W 15.85 ± 0.20 0.559 S 17.07 ± 0.20 0.519 W 17.64 ± 0.20 0.503 M18.68 ± 0.20 0.475 S 19.44 ± 0.20 0.456 W 19.78 ± 0.20 0.449 M 19.98 ±0.20 0.444 S 20.22 ± 0.20 0.439 W 21.30 ± 0.20 0.417 W 22.80 ± 0.200.390 M 23.06 ± 0.20 0.385 M 24.29 ± 0.20 0.366 W 24.99 ± 0.20 0.356 VS.


10. The molecular sieve of claim 9, wherein the molecular sieve has amole ratio of at least 10 of (1) silicon oxide to (2) an oxide selectedfrom boron oxide, aluminum oxide, gallium oxide, indium oxide, andmixtures thereof.